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NJC
Table 1 Reaction of 2-aminobenzonitrile 1a and CO2 in the presence of
various catalystsa
purchased from Tokyo Chemical Inorganic Co., Ltd. 2-Amino-
4,5-dimethoxybenzonitrile (99%) was purchased from Fluoro-
chem Ltd. 2-Amino-5-bromobenzonitrile (99%) was supplied by
J&K Scientific Ltd. Triethylamine (NEt3, 99%) was obtained
from Aladdin. The deuterated solvent (DMSO-d6) was obtained
from Cambridge Isotope Laboratories, Inc. All the chemicals were
commercially available and were used without further purification.
Catalytic reaction
Entry
Catalyst(s)
Yieldb (%)
As an example, the procedure using 2-aminobenzonitrile as the
substrate is described, and those for other substrates were
similar. In a typical experiment, 2-aminobenzonitrile (2 mmol,
0.2643 g), ZnI2 (0.6 mmol, 0.6384 g), NEt3 (2 mmol, 0.2024 g)
and 0.2 mL toluene were loaded into a 22 mL stainless-steel
batch reactor equipped with a magnetic stirrer. The air in
the reactor was removed by blowing CO2 through the reactor.
Then, the desired pressure of CO2 was charged into the reactor
and the reactor was sealed. The reactor was placed in an oil bath
at the desired temperature, and the mixture was stirred. After the
reaction, the excess CO2 in the reactor was released slowly.
Subsequently, 15 mL water was added to the reactor, and the
mixture was centrifuged to precipitate the product. The product
was then washed with tert-butyl methyl ether (3 Â 15 mL) and
ethyl alcohol (2 Â 15 mL) and dried at 90 1C for 3 h. Finally, the
mass of the product was measured by an electronic balance, and
the isolated yield was calculated from 2-aminobenzonitrile. The
purified products were characterized by NMR spectroscopy.
1H NMR and 13C NMR studies were carried out with a Bruker
NMR spectrometer with [D6]DMSO as the solvent.
1
2
3
4
5
6
7
8
—
ZnI2
NEt3
0
0
o1
15
3
20
25
1
Zn(OAc)2/NEt3
Zn(C6H11O7)2/NEt3
ZnCl2/NEt3
ZnBr2/NEt3
KI/NEt3
ZnI2/NEt3
ZnI2/NEt3
9
58
97
10c
a
Reaction conditions: 2 mmol of 1a, 2 mmol of NEt3, 0.6 mmol of
b
c
catalyst, 0.2 mL toluene, 1 MPa CO2, 30 1C, 6 h. Isolated yield. The
reaction time was 21 h.
dissociation capacity with Zn(II),25 which may increase the reactivity
of Zn(II). Thus, ZnI2 showed the highest catalytic activity, and the
ZnI2/NEt3 catalyst system could effectively promote the reaction,
affording a 97% yield of 2a within 21 h.
Effects of the reaction conditions
Subsequently, the effects of the molar ratios of ZnI2 and NEt3
on the reaction over the ZnI2/NEt3 system were also respectively
investigated, and the results are shown in Fig. 1. It was shown
that the yields depended strongly on the molar ratios of ZnI2
and NEt3. The yield could reach 97% at a ZnI2 molar ratio of
30% and a NEt3 molar ratio of 100%; this result indicated the
significant roles of ZnI2 and NEt3 in catalyzing the reaction.
We further studied the effects of CO2 pressure, and the
dependence of the yield of 2a on CO2 pressure is given in
Fig. 2a. As expected, the yield of 2a increased with increasing
CO2 pressure at the beginning, and a yield of 97% could be
achieved at 1 MPa CO2. No further increase in the yield was
observed with increased CO2 pressure, suggesting that 1a was
Results and discussion
Screening of catalysts
Firstly, the catalytic activities of various catalytic systems were
tested using the conversion of CO2 and 2-aminobenzonitrile
(1a) to quinazoline-2,4-(1H,3H)-dione (2a) as a model reaction
at 30 1C and 1 MPa CO2; the results are given in Table 1. It was
found that the reaction did not occur in the absence of any
catalyst (Table 1, entry 1), as well as in the presence of individual
ZnI2 or NEt3 (Table 1, entries 2 and 3). In the presence of NEt3,
different zinc salts, including Zn(OAc)2, Zn(C6H11O7)2, ZnCl2,
ZnBr2 and ZnI2, were also investigated, and all of them could
promote this reaction with yields of the target product 2a
ranging from 3% to 58% in 6 h (Table 1, entries 4–7 and 9).
Interestingly, the catalytic activities of the halogen-based zinc
salt/NEt3 systems were better than those of the oxygen acid-
based zinc salt/NEt3 systems, and the catalytic yields of the zinc
halides followed the order: ZnI2 4 ZnBr2 4 ZnCl2; this
indicates that the halide ions, especially IÀ, may be crucial for
the high catalytic activity of the zinc halide/NEt3 system. In
order to confirm the role of IÀ, the activity of a KI/NEt3 system
was also screened. However, the KI/NEt3 system had low catalytic
activity for the reaction (Table 1, entry 8). This result indicates
that compared with IÀ, Zn(II) plays a more important role in
this reaction. Compared with other halide ions, IÀ has stronger
Fig. 1 Dependence of the yield on the molar ratios of ZnI2 and NEt3.
Reaction conditions: (a) 2 mmol of 1a, 2 mmol of NEt3, 0.2 mL toluene,
30 1C, 1 MPa CO2, 21 h and different molar ratios of ZnI2; (b) 2 mmol of 1a,
0.6 mmol of ZnI2, 0.2 mL toluene, 30 1C, 1 MPa CO2, 21 h and different
molar ratios of NEt3. Isolated yields.
This journal is ©The Royal Society of Chemistry and the Centre National de la Recherche Scientifique 2019 New J. Chem., 2019, 43, 16164--16168 | 16165